Apparatus for treating crude oil vapors



May 3, 1949. A. v. B. CANDLER APPARATUS FOR TREATING CRUDE OIL VAPORS Fil ed July 19. 1945 5 Sheets-Sheet l IIIIIIIIIIII-IIIIIIIII AI ll I IIIIIII II IIII kiiii Illiilliili y 1949; A. v. B. CANDLER 2,468,958

APPARATUS FOR TREATING CRUDE OIL VAPORS Filed July l9, 1945 v 5 Shets-Sheet 2 May 3, 19 49.

A. V. B. CANDLER APPARATUS FOR TREATING CRUDE OIL VAPORS Filed July 19, 1945,

5 Sheets-Sheet 3 y 3, 9 A I v. B. CANDLER 2,468,958

APPARATUS FOR TREATING CRUDE OIL VAPORS Filed July 19, ,1945 5 Sheets-Sheet 4 y 9- A. v. B. CANDLER I 2,468,958

APPARATUS FOR TREATING CRUDE OIL VAPORS Filed July 19, 1945 5 Sheets-Sheet 5.

' Inu mtor.

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Patented May 3, 1949 APPARATUS FOR TREATING CRUDE OIL VAPORS Arthur V. B. Candler, Tulsa, Okla., assignor to Maloney-Crawford Tank & Manufacturing 00., Tulsa, Okla, a corporation of Delaware Application July 19, 1945, Serial No. 605,949

3 Claims.

My invention relates to apparatus for treatin crude oil containing an emulsion, to break the emulsion and free the oil, and also for separating out the free water and gas in the mixture.

Important objects of the invention are to modify or change the apparatus shown in my copending application for Method of and apparatus for treatin crude oil, filed December 1, 1944, Serial Number 569,190, and to provide an apparatus for meeting difierent conditions of service; to provide means for effectively dehydrating without evaporation losses where the crude emulsion contains only small volumes of free water and small volumes of gas, or where the free water has been removed prior to delivery of the crude emulsion to such apparatus; to provide apparatus of the above mentioned character for effectively dehydrating crude oil emulsions in which the gas liberated during the process is comparatively low in volume and also the free water is comparatively low in volume, while accomplishing the separation and maintaining the gravity and volume content of the oil contained in the emulsion; to provide apparatus of the above mentioned character, which is continuous and efiicient in operation; which has been found-to break tight petroleum emulsions without the aid of interposed filters; which will first separate the free water and gas from the emulsion and then treat the emulsion in order to lower the interfacial tension between the oil and water constituting the liquid and to remove solid particles, such as mineral salts, therefrom; which will subject the oil vapors to a treatment for separating the dry gas and liquid content from such vapors; which will produce a lowered temperature in the gas separating means to facilitate the separation of the liquid content; which will cause the emulsion to be continuously circulated in a body of water while being subjected to the action of heat and a retarding and rubbing action for breaking the tight emulsion; which will maintain substantially constant the level of the liquids being treated; and which has its several parts correlated for employing the action of heat, gravity, centrifugal force, gas expansion, condensation, reduction of velocity and surface contact, in its operation.

Other objects and advantages of the invention will be apparent during the course of the following description.

In the accompanying drawings forming a part of this application, and in which like numerals are employed to designate like parts throughout the same,

Figure 1 is a central vertical section through the upper portion of the apparatus embodying my invention,

Figure 1 is a similar view through the lower portion of the apparatus,

Figure 2 is a side elevation, parts in section, of the upper portion of the apparatus,

Figure 2 is a similar view of the lower portion of the apparatus,

Figure 3 is a horizontal section taken on line 33 of Figure 1, the main casin being omitted Figure 4 is a horizontal section taken on line 4-4 of Figure 1,

Figure 5 is a horizontal section taken on line 55 of Figure 1,

Figure 6 is an enlarged central vertical section through the gas separating chamber and associated elements,

Figure 7 is a horizontal section taken on line l'! of Figure 1 Figure 8 is an enlarged fragmentary section through the perforated cone or tapered plate,

Figure 9 is a plan view of the apparatus.

In the drawings, wherein for the purpose of illustration is shown a, preferred embodiment of my invention, the numeral 20 designates a vertical casing or tank, which is preferably cylindrical and closed at its top and bottom by heads 2| and 22.

The apparatus comprises a gas separating chamber or turret 23, and means are provided for forming within the tank 20 a receiving chamber 24, a settling chamber 25, a scrubbing and treating chamber 26, and a heating and bottom accumulator chamber 21. These various chambers are arranged in end-to-end superposed relation, as shown. The casing 20 is provided with tube gauges 28, indicating the level of th liquids in the several chambers.

The gas separating chamber or turret 23 has its lower end mounted upon the top of the receiving chamber 24, and extends below this top for a short distance. The chamber or turret 23 is provided with an annular imperforate bottom 29, Figures 4 and 6. Connected with the annular bottom 29 at its center is a large vertical tube or cylinder 30, the lower end of which is open, and in free communication with the receiving chamber 24. Arranged above the top of the central tube of cylinder 30 is an imperforate plate 3|, attached to the tube 39 and forming a gas-tight joint therewith. The plate 3| is circular and is arranged in spaced concentric relation to the side of the chamber or turret 23, as shown. The plate 3| is conical and tapers downwardly and has a 23, as shown. The annular bottom 29 and plate:

33 form an annular sump chamber. .andlthe lower end of the pipe 32 discharges into this sump chamber, at its inner periphery. The separated oil collected upon the topwof' the plate 3 will gravitate through the pipe 3? and be conducted into the sump chamber 3 ceiving space or chamber 35. The central tube 3!) is provided with openings 36, covered by wings or vanes 31, attached to the tube fit and to the plates 3! and 33. The-outerportions of these wings or vanes-arebent or'face circumferentially;

affording discharge openings 38, andthese wingsor vanes are adapted to impart 'a circumferential movement to the gases passing through andfrom' the openings 36.: Arranged between the pie-test l and 33 is a barrier or "obstructing unit including an annular set of verticalchannels 3B, which .iace

inwardly, and are attached to the-:plates 3i and;

are

33 at their peripheries; These channels spaced, providing passagese iii, Figure 3, in communication with-the spaceor. chamber 35, and an annular vertical passage 4|, Figures Land -6, which leads into the sump chamber 3d. The plate 33 is provided with an annular set of apertures- 42, leading intothe passageslof the: channels, as shown. Theplate 33 has additional aperturesth Apertures 2 and 413 are in communication with the sump chamber 34. Arranged within. the chamber or turret 23 above and spaced from the plate 35 is a conical or upwardly tapering plate Mi, extending to the side of the turret (iii-and attached thereto. This conical or tapered plate Mis perforated, as shown at 45; These perforations d5 are punched'and swaged inwardly or downwardly, as shown in Figure 8. The plate- M forms with the plate 3| a chamber M receiving the relatively cool drygas'from the gas separating section. It is pointed out thatthe temperature of the vapors released "from the hot oil in the settling chamber upon passing upwardly; through the pipes il which are-immersed in the relatively cool incoming emulsion" in receiving-v chamber 24, is progressively reduced due to the heat transfer between the warm vapors arising This" through pipes 41 and the cool emulsion. promotes separation of the heavier hydrocarbcns by condensation in addition to the mechan-' ical action of the gas separator; In the present apparatus, the gas separating chamber or turret 23 is in effect a separate unit, providing means. for reclaiming the liquid and'draining it directly into the settling chamber, which'means is not in the receiving chamber."

The receiving chamber 24 has a bottom which is conical or tapers downwardly. Vertical pipes 3'! pass through the annular bottom'Z'Q and.

through the plate 33 and lead into the chamber.

35, at their upper ends, and 'di'scharge'into'the. chamber 35, within the'wings or vanes 32. The

pipes tl correspond in number to the wings or The lower ends of the pipes' i'i passthrough the bottom 46 and lead into the top of' the settling chamber 25; Each-pipe i'l'hasits VGLIIBS 3 I.

opposite endsopen. verticali down pip'es as have The plate 3| forms with the plate 33 an annular gas re-- their upper ends leading into the sump chamber 34. These down-pipes 48 pass through the bottom 46 and discharge into the settling chamber 25, near its bottom. Two pipes 41 are shown for the purpose of illustration. The settling chamber 25 has a horizontal bottom d9, provided with a group of'apertureszifl; .astshown;

Th'eaemulsion' is'suppliedto the receiving chamber 24 through a pipe 5!, leading into the receiving chamber near its bottom and well below the level of the raw emulsion therein. The pipe 5| dischargesinto 'an' inlet diverting box or nozzle 52, arranged within and at the periphery of the chamber 44. Thisv diverting box or nozzle extends circumferentially of the periphery of the chamb'er'24 and will cause the infiuent to travel circumferentially of the chamber 24. The numeral 53 designates a receiving box, having its top open, and connected with the upper end of a vertical down-pipe 54 which extends downwardly into thezchamber 21-,- as shownt The receiver box 53 is arranged near the-upperendof the chamber 24- and determines the'level of the-emulsion there-- It ispointed out that the oil-inlet'for the in. reeciving chamber 24 -is submerged atall times,

facilitatingg preliminary stratification of free.

become entrained in the emulsion before enter-- ing. the receiving box 53,- while the freergas'libereated from'the emulsion :rises into: the separating:

chamber or turret ior' extractionof the heavier fractions, thereby eliminating-lossof-volume or reduction in gravity of the-treated product. The: settling chamber 25 hasianoutlet-pipe ElB, lead ing into the upper portion thereof, for determin ingithe level of the .pure oil' therein This outlet.-

Agas return: pipe'filrisconnected with-the: pipe 55 and leads-'1 back into" the top of the': settling chamber 2.5,

pipel'is connected with: a pipe 1 56 as shown;

The scrubbing'oritreating chamber 26 maybe.

regarded as :extending' fromethesbottom as; to

horizontaLseg-mental partitions 58, each or which extends for These segmental partitions are spaced for 90 affording open :vertical channelsor passages 59betweenthem. The-sides or these:

ch'annels59'are covered by depending aprons 6i],

curved inihorizontal cross section, and arranged at'the inner edges of the segmental partitions 58* extending for 90".

The segmental partitions 58:

and'aprons BU ar-e identical with the segmental partitions and aprons disclosed in my said co-" pending application.

Arranged'within the chamber 26 are spaced baffle trays are-identical in construction and arrangement with-th'e'b'afile trays-shbwnin my said co-pending application,- andth'e uppermost bafllespacedhorizontalbranch pipes in: These'branch" pipes are apertured or havenozzles upon-theirtop sides, for spraying the emulsion upwardly.

This spreader is identical with the spreader shown in my-said"co-pending-application;

The numeral H designates a heating element, identical: with the heating element shown in my said co pending application. This heating ele-' ment projects into the ch'amber fl abovethe' ipes' 69 and 10. The heating element includes 'a' cen ment for water disposal.

nected with the salt water disposal pipe '13.

tral tube and an annular group of tubes, for the passage of the products of combustion. The liquid within the chamber 21 is heated by the heating element and passes upwardly within the chamber 21 about and in contact with the heating element. A differential pressure control device is provided for the outlet pipe 56 and includes a diiierential pressure operated valve l2 connected in the pipe 56. When the valve 12 opens, the oil is withdrawn. This valve includes a valve element connected with a diaphragm. This differential pressure valve is identical with the differential pressure valve controlling the outlet of the oil in my said co-pending application.

The numeral 13 designates a drain pipe having a branch M connected with the head 22 and leading into the bottom of the chamber 2i. The pipe 13 is equipped with a valve 15. Connected with the drain pipe 13 is a branch pipe 76, equipped with a cut-01f valve TI. connected with the bottom 4B of the chamber 24. By opening the valve 55, the chambers 25 and 2'! may be drained, and by opening the valve 11, the chamber 24 may be drained. When the valve 11 is opened, the bottom of the chamber 2:3 is placed in communication with the automatic siphon draw-off pipe 13, so that the water in the bottom of the chamber E l may be manually drained as required.

Means are provided for maintaining a selected level of the salt water within the chambers 26 and 2?, including the conventional siphon arrange- This means includes a vertical pipe 78 extending into the casing 26 and having its intake end terminating near the bottom of the chamber 2?. ,The upper end of this pipe is connected with a siphon box Figure 2, connected at its top with a pressure equalizer pipe 86, leading into the chamber 25. Ex-

tending into the box 19 is a vertically adjustable pressure valve 83 connected therein and this differential pressure valve is identical with the coraresponding differential pressure valve shown in my co-pending application. The pipe 32 is con- A pipe 84 is connected with the chamber or turret 23, and has a pressure relief valve 85 connected therein. This is a safety valve and opens only at a pressure above the selected operating pressure to be carried in the apparatus. A pipe 86 is connected with the pipe 84'. and has a back pressure regulator valve 8'! connected therein. This regulator valve has a diaphragm which opens and closes thevalve element in response to small variations in inlet pressure, thereby automatically maintaining the selected operating pressure to be carried. The valve 81 is identical with the corresponding valve used in my said co-pending application. A (pipe 88 is connected in the pipe 86 and is connected with a branch pipe 89, which is connected with the diaphragm housing of the valves 12 and 83 above the diaphragms therein. The pipe 88 and branch pipe 89 are small gas equalizing lines to convey the pressure maintained in the system including gas disposal pipe 86, to the top of diaphragms in differential control valves, on both the water disposal and oil discharge lines. The action of these two difierential control valves is responsive to the hydrostatic This branch pipe it is iii 6. head of the liquid in the salt water disposal line' 82 and in'the oil discharge pipe 56, which acts upon the diaphragms of the valve 83 and (2, unseating the valve elements in opposition to the action of the valve counter-balance weights. Since the weight of the valve elements including diaphragm, plate, stem and the force created by the constant gas pressure on top of the diaphragm, is just counter-balanced by means of the Weight and lever, the valve opens and closes responsive to the column of fluid in the draw-off lines independently of any change of pressure in the system or head of fluid existing in the treater proper.

The operation of the apparatus is as follows:

The crude oil having the free water previously removed therefrom or containing the emulsion and a relatively small amount of salt water and gas is fed continuously at the proper rate through the pipe 5| into the diverting box or nozzle 52, within the receiving chamber 24. The result of the circumvolution of the liquid in the chamber 24 tends to the separation of the relatively small amount of free gas associated with the emulsion. The chamber 24 is filled with the emulsion to the level of the receiver box 53, and the level is maintained at this elevation of the receiver box, and the emulsion flows into the top of the receiver box 53 and then into the down-pipe 54. The small amount of free water associated with the emulsion settles in the bottom of the receiver chamber, M. The free gas released within the receiver chamber 24 passes upwardly through the central tube 3d. This gas passes radially through the openings 36 and discharges within'the wings or vanes 31 within the chamber 35 and mingles with the gas discharging from the upper ends of the pipes 41 from the top of the settling chamber 25.-

These gases contact with and rub against wings 31 and adjacent walls and travel circumferentially within these wings and then discharge into the space inwardly of the channels 39 and contact with and rub against these channels. The gases then pass between the channels and enter the passage 4! and pass upwardly into the chamber 44' beneath the apertured plate li and contact with and rub against the lower surface of this apertured plate. The apertures of this plate are punched and swaged downwardly, as stated. The gases then discharge through the apertures 45 into the upper portion of the chamber or turret 23. This contacting and rubbing action separates the oil mixed in the gas stream. The dry gas passes out through the outlet pipe 86. The heavier hydrocarbons or oil mixtures are now converted into liquid form and this liquid oil within the chamber M beneath the apertured plate Mis partly caught upon the upper surface of the plate 3| and partly descends through the passage 4!. This oil is conducted through the pipe 30 and passage M to the sump chamber 34, and is conducted bythe down-pipes 38 into the bottom of the. settling chamber 25. The lower ends of these pipes 48 form a liquid seal with the treated oil within the settling chamber.

Due to the low temperature in the chamber Ml and above it, there is a tendency to condense the heavy hydrocarbon fractions, as isopentanes, pen.- tanes and other heavier fractions, which otherwise would not be recovered by the mechanical action of the gas separator.

The emulsion entering the receiver box 53 now passes through the down-pipe 54. The emulsion flows by gravity through the pipe 54 and is discharged from the lower end of the down-pipe into the spreader, which-isslocatedbeneath the heating element "H. The warm gases released from the oil in the settling chamber .passup through the pipes '41 intowthe chamber .35, as stated.

The spreader now receives the descending emulsion and serves .to discharge vor .difiuse the emulsion over practically theerrtire cross-sectional area of the baflie trays. "This lemu'lslonlis sprayed from the spreader in an-upwardsdirection and the warm emulsion rises and flows upwardly around the heating element and is heated thereby. The flow of theemulsion'through theapertures or nozzles of the pipes 10 is maintained constant by the static head created by the nominal distance between the receiver boxw58 .and the. spreader.

The emulsion therefore discharges from the spreader upwardly in a continuous manner and passes around and in contact with the heating element. The heated emulsion .passes upwardly above the heating element andis restricted .in its upward passage upon entering the scrubbing and treating chamber '26 :where it engages with scrubbing trays.

The upwardly traveling emulsion .enters the bottom baffle tray El and then passes from this baffle tray to and through each succeeding upper bafile tray. In passing througheach baflle tray, the velocity of the emulsion is reduced. The emulsion is caused to travel horizontally in a tortious passage about .the .bafiles in each baffle tray, and travels in .oppositeldirections in each succeeding baifle :tray, as fully disclosed in my said co-pending application. :By this arrangement, the horizontal and vertical travel of the emulsion is prolonged and :this produces an optimum of scrubbing and washing I efiect. The fluid, owing to its slow passage through the arrangement of baffle trays, rises by thermoaction and the oil is released by gravitational separation, the result of heating and scrubbing contact that the emulsion had with the baflies and baffie ltrays. The mixture, in its circuitous upward travel, contacts With the lower races of the baille trays, marginal flanges and .baffles, andthe droplets of oil are slowly pushed along in :the fluid stream, while impinging against the surfaces. This scrubbingaction under :the application of heat lowers the interfacial tension between the oil and brine surfaces, thereby separating the oil. from the salt water and from any free salt or solids in suspension. In passing under the trays, the oil in the fluid stream being at the top,and the salt water and heavier constituents,- at -the bot tom, these heavier constituents are drawn off under each baflie tray, such heavier'constituents moving outwardly and downwardly between the marginal flange of each baflie tray. and reflux from beneath the marginal flange. The salt Water and heavier constituents, upon passing-out.- wardly beyond the marginal flanges of the baflie trays, enter the vertical passage which surrounds these trays and travels downwardly and in this passage, by gravity, will-impingeupon the segmental partitions 58, and are deflected thereby into the open vertical passages-5'9. *In passing downwardly through the passagesfiB, the aprons 6B tend to separate the downwardly -movi-ng salt water and the heavy constituents from the upwardly moving emulsion discharging from the spreader. The several baflle trays forming the baflleunit are so spaced that they provide side opening areas for effecting a refluxing of -the salt Water and heavy constituents-without the use of a central pipe. The relationship of the --baflle unit and the'heating element is ,of prime considr eration, in that these two elements, in conjunction with the arrangement of the passages formed by the segmental partitions .58 and aprons :50, pro.- vide a means that results in an extremelyefficient circulating system. The level of the water in the chamber '27 is maintained constant .by the adjustable siphon.

The oil released from the mixture as it rises through the trays, spreads out in a thin-film under the tray-heads, while the salt Water and heavier constituents descend as reflux. The scrubbing and washing action frees the oil of impurities and solids, such as salt particles held in suspension, and the clean oil, after passing through the perforations 5|], travels through the body of oil collected in the settling chamberrgZfi. As the gas liberated from the oil .on'its passage in and from the baflie unit and through the settling chamber tends to turbulence, for this reason the apertures 59 are arranged with respect to apertures 68, to direct the .oil cross-wise from the apertures 68 to the apertures 58, which causes further retardation of the flow of theoil in th settling chamber and prevention of intense ebullition of the gas. As the level of .oil rises in the settling chamber, the treated .oil passes through pipe 55. Any warm .vapors released in the settling chamber 25 pass upwardly through the pipes ll, as explained.

Under operation, a constant pressure is carried throughout the system while automatic discharge of both the .oil and salt water is governed by the difierential control valves '72 and :83. The gas pressure is maintained constant and equal upon the upper side of the diaphragms of these differ. ential control valves. The hydrostatic head .of the liquid in the salt water outlet pipe-8.2 and in the oil outlet pipe 56 acts upon the lower faces of the diaphragms and unseats the valve elements in opposition to the action of the Weights, and since the weight .of the valve element includes diaphragm, plate, and stem and the force created by the constant gas pressure .on the top of the diaphragm are just counterbalanced by 'meansof the weight and lever, the valve opens and closes responsive of the column of fiuid in the draw-off lines, independently of any change of pressure in the system or the head of fluid existing in the treater proper. It is preferred to operate the apparatus under a pressure of from ten tofifteen pounds per square inch, in which case the dif. -ferential controls are necessary.

In case it is desired to handle emulsions at or near atmospheric pressure, in order to take off the gas in receivin chamber 24, rather than :to :handle volatile gases in connection with gaseous fluids released when heating under pressure, then the regulating differential pressure valves 12 and 33 and the back pressure regulator valve 8'! are not required. The relief valve d5 may also be dispensed with, although it may be advisable :to employ a relief valve with an outlet range in ounces of pressure, to meet various conditions of service, as an excessive flow rate.

It is preferred to maintain the temperature within the chambers 35 and .2? to a degree sufii- .cient to break the emulsion but w-ithinlirnits, not enough to cause excessivevaporization of the -oil. The average temperature is about F., although this may be varied as found advantageous. A self-acting temperature controller for automatically regulating thegas burner to maintain a constant predetermined temperature is employed for efficient operation. A thermometer, indicating pressure gauge, and liquid level gauge graph are also generally used.

It is to be understood that the forms of my invention herewith shown and described are to be taken as preferred examples of the same, and that various changes in the shape, size and arrangement of parts may be resorted to without departing from the spirit of my invention or the scope of the subjoined claims.

Having thus described my invention, what I claim is:

1. Apparatus for treating crude oil vapors, comprising an upstanding separating chamber, an upstanding central tube extending through the bottom of the separatin chamber and spaced from the side of the separating chamber, the central tube having spaced openings in its side, an imperforate plate provided at the top of the central tube and the openings of the central tube and extending radially beyond the central tube for a substantial distance and spaced from the side of the separating chamber, a second plate surrounding the central tube beneath the open ings and forming a space with the upper imperforate plate and spaced from the bottom of the separating chamber for forming a sump chamber, the lower plate being spaced from the side of the separating chamber, vanes disposed within the space between the upper and lower plates and including inner generally radial portions disposed adjacent to and upon corresponding sides of the openings of the central tube and outer circumferential portions which extend in the same direction and cover the openings of the central tube for imparting a generally horizontal circumferential movement to the vapors discharging through such openings, a plurality of outer tubes having substantially vertical discharge ends for discharging the vapors upwardly and substantially vertically through the lower plate and within the space and vanes at substantially right angles to the horizontal discharge of the vapors through the openings of the central tube, means to supply vapor to the central tube, means to supply the vapor to the outer tubes, and means providing gas and oil outlets from the apparatus.

2. Apparatus for treating crude oil vapors, comprisin an upstanding separating chamber, a relatively large upstanding central tube within the separating chamber and having spaced openings in its side, an imperforate conical downwardly tapering plate covering the upper end of the central tube and disposed above the openings in the central tube and extending radially beyond the central tube for a substantial distance and spaced from the side of the separating chamber, a second plate surrounding the central tube beneath the openings and forming a generally horizontal space with the upper imporforate plate and spaced from the bottom of the separating chamber for forming a sump chamber, the lower plate being spaced from the side of the separating chamber and having openings provided near and. corresponding in number to the openings of the central tube, vanes disposed within the space between the upper and lower plates and including generally radial inner portions disposed adjacent to and upon corresponding sides of the openings of the central tube and the openings of the lower plate and outer circumferential portions which extend in the same direction and cover the openings of the central tube for imparting a generally horizontal circumferential movement to the vapors discharging through such openings, a plurality of outer tubes having substantially vertical discharge ends for discharging the vapors upwardly and substantially vertically through the openings in the lower plate and Within the space and vanes at substantially right angles to the horizontal discharge of the vaporsthrough the openings of the central tube, means to supply vapors to the central tube, means to supply vapors to the outer tubes, a tube connected with the lower end of the conical plate and passing through the central tube and discharging into the sump chamber, and means providing as and oil outlets from the apparatus.

3. Apparatus for treating crude oil vapors, comprising an upstanding separating chamber, an upstandin central tube within the separating chamber and having spaced openings in its side, an imperforate upper plate provided at the top of the central tube and the openings of the central tube and extending radially beyond the central tube for a substantial distance and spaced from the side of the separating chamber, a second plate surrounding the central tube beneath the openings and forming a generally horizontal space with the upper plate and spaced from the bottom of the separating chamber for forming a sump chamber, the lower plate being spaced from the side of the separating chamber and having openings provided near and corresponding in number to the openings of the central tube, separate circumferentially spaced vanes disposed within the space between the upper and lower plates, each vane including an inner generally radial portion disposed adjacent to and upon one side of the opening of the central tube and the opening of the lower plate and an outer circumferentially extending portion which covers the opening in the central tube, the circumferentially extending portions being spaced from each other and extending in the same direction, a plurality of outer tubes having vertical discharge ends discharging upwardly through the openings in the lower plate, the arrangement being such that the vapors from the outer tubes pass into the vanes at right angles to the vapors from the openings of the central tube, means to supply vapors to the central tube, and means to supply vapors to the outer tubes, and means providing gas and oil outlets from the apparatus.

ARTHUR V. B. CANDLER.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 668,866 Young Feb. 26, 1901 970,477 Drum Sept. 20, 1910 1,770,773 I-Iackett July 15, 1930 1,970,783 Walker Aug. 21, 1934 2,016,642 Lincoln Oct. 8, 1935 2,167,160 Raymond July 25, 1939 2,197,189 Morgan Apr. 16, 1940 2,232,948 Ihrig et al., Feb. 25, 1941 2,256,524 McKelVey Sept. 23, 1941 2,384,222 Walker Sept. 4, 1945 

